Process for preparing an oxime a structured catalyst including microporous oxides of silicon, aluminum and titanium

ABSTRACT

A catalyst includes or consists essentially of the oxides of silicon, aluminum and titanium, characterized in that the catalyst particles are built up from a core with the composition (SiO 2 ) y  (AlO 2 ) y  M y , wherein x/y=10 to ∞ and M=H, Na, K, NH 4 , or NR 4 , wherein R is a C 1-8  -alkyl, and a shell with the composition (SiO 2 ) n  (TiO 2 ) m , wherein n/m=12 to 1000. Both the core and the shell have a crystal structure of MFI or MEL. The catalyst can be prepared by preparing a synthesis gel for the preparation of a titanium silicalite, thereafter introducing an aluminosilicata of the MFI or MEL structural type into this synthesis gel, and working up the synthesis gel in a known manner to obtain the product.

This application is a divisional of application Ser. No. 08/274,198filed on Jul. 12, 1994, now U.S. Pat. No. 5,525,563 which application isentirely incorporated herein by reference.

BACKGROUND OF THE INVENTION

The invention relates to a structured catalyst including microporousoxides of silicon, aluminum and titanium, and a process for producingthis catalyst.

Microporous aluminosilicates of the structural type MFI (ZSM-5) and MEL(ZSM-11), and methods for producing them by hydrothermal synthesis areknown from U.S. Pat. No. 3,702,886 and DE 21 19 723. These patentdocuments are entirely incorporated herein by reference. The structuraltypes MFI and MEL are also described in W. M. Meier and D. H. Olson,Atlas of Zeolite Structure Types, Butterworth-Heinemann, 1992, which isalso entirely incorporated herein by reference. Aluminum-free materialswith identical structures, known as silicalite-1 and silicalite-2, aredisclosed in U.S. Pat. No. 4,073,865; U.S. Pat. No. 4,061,724; D. M.Bibby, N. B. Milestone, and L. P. Aldridge, Nature 280, 664 (1979); andEuropean Patent Appl. No. 112,006. These documents also are entirelyincorporated herein by reference. Materials in which some of the siliconatoms in the silicalite-1 or silicalite-2 structures are replaced bytitanium atoms are known as titanium silicalites TS-1 and TS-2 and aredescribed in DE 30 47 798 and J. S. Reddy, R. Kumar, and P. Ratnasamy,Appl. Catal., 58 (1990) L1-L-4. These documents also are entirelyincorporated herein by reference. Titanium silicalites are efficientcatalysts for selective oxidation using hydrogen peroxide, in particularfor the epoxidation of olefins (European Patent Appl. No. 100,119), thehydroxylation of aromatic compounds (DE 33 09 669 and J. S. Reddy, R.Kumar, and P. Ratnasamy, Appl. Catal., 58 (1990) L1-L4), thehydroxylation of aliphatic compounds (European Patent Appl. No. 412,596and J. S. Reddy, S. Sivasanker, and P. Ratnasamy, J. Mol. Catal., 70(1991) pp. 335-342) and the ammoximation of cyclohexanone (EuropeanPatent Appl. No. 208,311 and J. S. Reddy, S. Sivasanker, and P.Ratnasamy, J. Mol. Catal., 69 (1991) pp. 383-392). All of thesedocuments are entirely incorporated herein by reference.

The known preparation of titanium silicalites TS-1 and TS-2 proceeds viaa two-stage synthesis. First, a gel is produced by hydrolysis of asource of titanium, such as TICl₄, TiOCl₂ or Ti(Oalkyl)₄, preferablyTi(Oalkyl)₄, and a source of silicon, such as silica gel or Si(Oalkyl)₄,preferably Si(Oalkyl)₄. Then this gel is crystallized in a hydrothermalsynthesis by heating under pressure, wherein a template has to be addedto promote crystallization, such as tetra-n-propylammonium hydroxide forTS-1 or tetra-n-butylammonium hydroxide for TS-2. The high price ofTi(Oalkyl)₄, Si(Oalkyl)₄ and the templates contribute greatly to thecost of producing TS-1 and TS-2.

The titanium silicalites TS-1 and TS-2 are mostly produced in the formof small crystallites with sizes of less than one micrometer in theknown processes. These crystallites can only be separated from theliquid with difficulty by filtering. For industrial application of thesematerials, therefore, an additional agglomeration step is required. Anexample of such an agglomeration procedure is described in EuropeanPatent Appl. No. 203,260, which document is entirely incorporated hereinby reference.

When using titanium silicalites TS1 and TS2 as catalysts for oxidationreactions using hydrogen peroxide, the catalytic activity is determinedby the molecular size and molecular structure of the compound to beoxidized (M. Clerici and P. Ingallina, J. Catal., 140 (1993) pp. 71-83,which document is entirely incorporated herein by reference). Thisindicates that there is a restriction on the catalytic activity due tomaterial transport inside the cavities in the crystal lattice, so thattitanium atoms in the interior of the crystal contribute less to thecatalytic activity than titanium atoms near the surface of the crystal.

There is a need, therefore, for catalysts which exhibit similar activityto titanium silicalites in selective oxidation reactions using hydrogenperoxide, and which can be prepared using small amounts of Ti(Oalkyl)₄,Si(Oalkyl)₄, and a template, and which enable targeted setting of thecrystal size to enable better utilization of the catalytic activity ofthe titanium atoms.

SUMMARY OF THE INVENTION

The invention provides a catalyst including oxides of silicon, aluminumand titanium which is characterized in that the catalyst particles arecomposed of a core with the composition (SiO₂)_(x) (AlO₂)_(y) M_(y),wherein x/y=10 to ∞ and M=H, Na, K, NH₄, or NR₄, wherein R=C₁₋₈ -alkyl,and a shell with the composition (SiO₂)_(n) (TiO₂)_(m), whereinn/m=12-1000, and both the core and the shell have a crystal structure ofthe MFI or MEL type.

In preferred forms of the invention, the catalyst consists of orconsists essentially of oxides of silicon, aluminum and titanium.

In particularly preferred embodiments of the invention, the shell on thecatalyst has the composition (SiO₂)_(n) (TiO₂)_(m) wherein n/m=20-200.

The catalyst according to the invention can be prepared by preparing asynthesis gel in the same way as is known for preparing titaniumsilicalite (as shown, for example, in DE 30 47 798 and Reddy et al.,supra.), wherein a source of titanium, such as TiCl₄, TiOCl₂ orTi(Oalkyl)₄, and a source of silicon, such as silica gel or Si(Oalkyl)₄,can be mutually hydrolyzed; a tetraalkylammonium hydroxide can be addedas a template; a crystalline aluminosilicate, for example, one havingthe crystal structure of MFI or MEL, such as zoolite ZSM-5 or ZSM-11,can be introduced into this synthesis gel; and the synthesis gel can beworked up in a known manner to obtain the product, for example bycrystallizing under hydrothermal conditions, separating, filtering andcalcining the crystalline product.

The crystalline aluminosilicate can be added to the raw materials beforegel formation, or during the gel formation phase, or to the finished gelbefore crystallization. When adding the aluminosilicate in theprotonated H-form (H-ZSM-5 or H-ZSM-11), this, as an acid component, caninitiate precondensation.

BRIEF DESCRIPTION OF THE DRAWINGS

The invention will now be described in more detail using severalspecific examples, which are advantageously considered in conjunctionwith the attached drawings, wherein:

FIGS. 1a and 1b show scanning electron microscope (SEM) images of thecatalyst particles of Example 1 magnified 3000:1 and 10,000:1,respectively;

FIGS. 1c and 1d show scanning electron microscope images of the H-ZSM-5core material used in Example 1 magnified 3000:1 and 10,000:1,respectively;

FIGS. 2-5 show X-ray diffraction diagrams for the materials of Examples1-4, respectively;

FIG. 6 is a transmission electron microscope (TEM) image of a section ofthe catalyst particles according to Example 1, with an E-magnificationof 20,000 and a total magnification of 100,000:1; and

FIG. 7 is a transmission electron microscope image of a section of thecatalyst particles according to Example 3, with an E-magnification of12,000 and a total magnification of 50,000:1.

DETAILED DESCRIPTION OF THE INVENTION

The invention will now be described in more detail with the aid of theattached drawings and various specific examples.

A catalyst is provided in accordance with the invention which includesoxides of silicon, aluminum and titanium. The catalyst particles arecomposed of a core having the following composition:

    (SiO.sub.2).sub.x (AlO.sub.2).sub.y M.sub.y,

wherein x/y is in the range of 10 to ∞, and

M represents a member selected from the group consisting of H, Na, K,NH₄, and NR₄, wherein R in the formula "NR₄ " represents an alkyl having1-8 carbon atoms (i.e., a C₁₋₈ -alkyl).

The catalyst particles further include a shell having the followingcomposition:

    (SiO.sub.2).sub.n (TiO.sub.2).sub.m,

wherein n/m is in the range of 12 to 1000. Both the core and the shellhave a crystal structure of the MFI or MEL type.

In one particularly preferred embodiment of the invention, the core ofthe catalyst has the composition (SiO₂)_(x) (AlO₂)_(y) M_(y), whereinx/y is in the range of 10 to ∞, and the shell has the composition(SiO₂)_(n) (TiO₂)_(m), where n/m is in the range of 20 to 200.

The invention also relates to a process for preparing the catalysthaving the above-described characteristics. The process for preparingthe catalyst includes preparing a synthesis gel for the preparation of atitanium silicalite in a manner that is known in the art. A crystallinealuminosilicate is introduced into this synthesis gel, and the synthesisgel is worked up in a known manner to obtain the product.

In another aspect of the invention, after calcining the catalyst duringpreparation thereof, the catalyst is neutralized with a base whosepK_(S) value is between 0 and 11, so that an aqueous suspension of thecatalyst has a pH between 5 and 9 after neutralization.

Using the catalyst in accordance with the invention, an epoxide may beprepared by reacting an olefin with hydrogen peroxide in the liquidphase in the presence of the catalyst, and thereafter recovering theepoxide product. Likewise, the catalyst in accordance with the inventionmay be used in a process for preparing an oxime by reacting a ketonewith hydrogen peroxide and ammonia in the liquid phase in the presenceof the catalyst, and thereafter recovering the oxime product.

The composition of the synthesis gel for preparing the catalyst asdescribed above, can be selected to provide the following ranges ofmolar ratios:

SiO_(2/) TiO₂ =5-1000;

OH⁻ /SiO₂ =0.1-1.0;

H₂ O/SiO₂ =15-200, preferably 20 to 200; and

NR₄ ⁺ /SiO₂ =0.1-2.0.

The ratio of the amount of SiO₂ and TiO₂ contained in the synthesis gelto the amount of crystalline aluminosilicate added to the synthesis gelcan be selected to be within the range of 0.02 to 20 by weight.

The catalyst particles prepared in this way show the same morphology andparticle sizes as the aluminosilicate added as the core material in ascanning electron microscope image. The average particle diameter islarger than that of the titanium silicalite which is prepared in theabsence of the core material. Their X-ray diffraction diagrams, as shownin FIGS. 2 to 5, show the characteristic reflections for crystallinezeolites of the MFI structural type. The bands observed at 960-975 cm⁻¹in the IR spectrum demonstrate the incorporation of isolated titaniumatoms into the crystal lattice of the material.

Transmission electron microscope images of sections of the catalystparticles according to the invention (FIGS. 6 and 7) show the structureof the catalyst particles consisting of a closed shell on the corematerial used. X-ray photoelectron spectroscopy (XPS) of the catalystparticles shows that the surface of the catalyst particles contains onlytitanium and silicon, and no aluminum. After wearing away some of thecatalyst surface by sputtering, the amount of titanium detected by XPSdecreases considerably, and the aluminum contained in the core of theparticles is detected. This indicates that the catalysts according tothe invention have a structure comprising a core which essentially hasthe composition of the aluminosilicate used to prepare the catalyst, anda shell with the composition (SiO₂)_(n) (TiO₂)_(m).

The invention has the advantage, as compared with the prior art, that,in the catalyst according to the invention, the catalytically activetitanium atoms are intentionally incorporated into a layer at thesurface of the crystal, wherein the thickness of this layer can becontrolled by selecting the conditions of preparation. The requirementfor expensive starting materials is reduced, as compared with the priorart, due to this method of preparation. By using initial crystals ofspecific sizes, larger catalyst particles can be produced withoutadditional agglomeration steps, the size of the catalyst particles beingpredetermined by selecting the size of the initial crystals andselecting the conditions of synthesis.

The catalyst according to the invention can be used for selectiveoxidation using H₂ O₂ in the liquid phase, for example for ammoximationof ketones, such as cyclohexanone or cyclododecanone, or for theepoxidation of olefins, such as propene, 1-butane, 2-butane, 1-pantene,allyl chloride or allyl alcohol. The products from such reactions can berecovered in any conventional manner known to those skilled in the art.

When used to prepare acid-sensitive products, such as epoxides, thecatalyst can be neutralized after calcination by treating it with a basehaving a pK_(B) value between 0 and 11, preferably an aqueous solutionof sodium acetate, sodium carbonate, sodium bicarbonate or ammonia, sothat an aqueous solution of the catalyst after neutralization has a pHbetween 5 and 9.

EXAMPLES

The invention will now be described in various specific Examples. TheseExamples should be construed as illustrating the invention, and not aslimiting the same.

Preparation of the catalyst Example 1

37.2 ml of Si(OEt)₄ are diluted with 44.4 ml of absolute i-propanol in astirred flask (500 ml) provided with a stirrer, thermometer and refluxcondenser. The admission of atmospheric moisture into the flask isprevented by a CaCl₂ tube. Then 2.8 ml of Ti(O n-Bu)₄ in 8.5 ml ofabsolute i-propanol at room temperature are added dropwise withstirring. Finally 23.8 g of H-ZSM-5 (SiO₂ /Al₂ O₃ =67, d₅₀ =7.6 μm),which was first calcined at 550° C. for 1 hour, is added. The resultingsuspension is heated for two hours under reflux. After cooling to roomtemperature, 42.5 ml of a 20 wt. % strength aqueous solution oftetra-n-propylammonium hydroxide are added dropwise over the course of10 minutes, wherein the mixture warms up slightly. The flask is thenprovided with a distillation bridge. The mixture of alcohols,i-propanol, ethanol, n-butanol, and some water, are distilled off. 86 mlof water is added to the resulting residue and agitated. To crystallize,this mixture is transferred to an autoclave (500 ml) provided with astirrer and lined with Teflon® (a polytetrafluorethylene coatingavailable from the E.I. DuPont de Nemours Company) and heated to 180° C.for 22 hours. The solid obtained is isolated by centrifuging, washedwith two portions of 50 ml of distilled water, dried at 120° C. andcalcined at 550° C. for 10 hours. Finally, the product is treated for 1hour at 80° C. with 150 ml of a 10 wt. % aqueous ammonium acetatesolution, centrifuged off, washed with two portions of 50 ml ofdistilled water, dried at 120° C. and calcined at 550° C. for 10 hours.

The composition of the catalyst prepared in this way, determined by wetanalysis, is: TiO₂ : 1.6 wt. %; SiO₂ : 96.8 wt. %; and Al₂ O₃ : 1.6 wt.%.

The X-ray diffraction diagram (FIG. 2) shows that the catalyst consistsof crystalline material of the MFI structural type.

The IR spectrum shows a shoulder at 965 cm⁻¹, which is characteristic ofthe incorporation of isolated titanium atoms into the crystal lattice ofthe material. The scanning electron microscope image of the catalystparticles (magnification 3000:1 (FIG. 1a) and 10,000:1 (FIG. 1b)), ascompared with the scanning electron microscope image of the H-ZSM-5 corematerial used (magnification 3000:1 (FIG. 1c) and 10,000:1 (FIG. 1d)),show that the morphology and particle size of the core material isessentially retained during preparation of the catalyst.

The transmission electron microscope sectional image of a catalystparticle (FIG. 6, magnification 100,000:1) shows a structure having a0.08-0.15 μm thick, closed shell on the core material.

The surface composition (Si: 30.8 mol. %; Ti: 0.48 mol. %; and Al: notdetectable), determined by X-ray photoelectron spectroscopy (XPS),indicates that the shell of the catalyst consists of aluminum-freetitanium silicalite. The surface composition found after wearing awaythe surface by means of sputtering (Si: 34.7 mol. %; Ti: 0.19 mol. %;and Al: 0.80 mol. %) indicates that the titanium is essentiallycontained only in the shell and not in the core of the catalyst.

Example 2

Example 1 is repeated with the difference that 17.8 g of H-ZSM-5 (SiO₂/Al₂ O₃ =150, d₅₀ =5.7 μm) is used.

The composition of the catalyst prepared in this way, determined by wetanalysis, is: TiO₂ : 2.3 wt. %; SiO₂ : 96.9 wt. %; and Al₂ O₃ : 0.8 wt.%.

X-ray diffraction diagram: FIG. 3.

IR spectrum: shoulder at 966 cm⁻¹.

Example 3

Example 1 is repeated with the difference that 53.5 g of H-ZSM-5 (SiO₂/Al₂ O₃ =ca. 1000, d₅₀ =16.1 μm) is used.

The composition of the catalyst prepared in this way, determined by wetanalysis, is: TiO₂ : 0.6 wt. %; SiO₂ : 99.3 wt. %; and Al₂ O₃ : 0.1 wt.%.

X-ray diffraction diagram: FIG. 4.

Transmission electron microscope sectional diagram (magnification50,000:1): FIG. 7.

Example 4

Example 1 is repeated with the difference that 11.2 g of H-ZSM-5 (SiO₂/Al₂ O₃ =28, d₅₀ =3.7 mm) is used.

The composition of the catalyst prepared in this way, determined by wetanalysis, is: TiO₂ : 3.3 wt. %; SiO₂ : 93.5 wt. %; and Al₂ O₃ : 3.2 wt.%.

X-ray diffraction diagram: FIG. 5.

IR spectrum: band at 972 cm⁻¹.

Example 5 (Comparison Example)

A non-structured, pure titanium silicalite was synthesized in accordancewith Example 1 of German Patent DE 30 47 798 as a comparison catalyst.

The composition of the catalyst prepared in this way, determined by wetanalysis, is: TiO₂ : 2.5 wt. %; and SiO₂ : 97.5 wt. %.

The following are examples of the ammoximation of cyclohexanone to givecyclohexanonoxime using the catalyst compositions produced above.

Example 6

1.0 gram of catalyst in accordance with Example 1 was initiallyintroduced into a mixture of 17 ml of tert-butanol and 20.5 ml of 14 wt.% strength aqueous ammonia solution in a 100 ml reactor with adouble-walled jacket and a pressure retention device. After sealing theapparatus, it is heated to 80° C., and 7.16 ml of cyclohexanone and 7.27ml of 30% strength aqueous hydrogen peroxide solution are addedsimultaneously, with stirring, over the course of 5 hours. The mixtureis subsequently stirred for 30 minutes at 80° C., then cooled to roomtemperature, the pressure is released, it is diluted with tert-butanoland filtered. Unconverted hydrogen peroxide is determined by iodometrictitration, unconverted cyclohexanone and the cyclohexanonoxime producedare determined using gas chromatography. With a hydrogen peroxideconversion of 99% and a cyclohexanone conversion of 94%,cyclohexanonoxime is formed with a selectivity of greater than 99%, withreference to the cyclohexanone converted.

Example 7

Example 6 is repeated with 1.0 gram of catalyst in accordance withExample 2. With a hydrogen peroxide conversion of 100% and acyclohexanone conversion of 79%, cyclohexanonoxime is formed withgreater than 99% selectivity, with reference to the cyclohexanoneconverted.

Example 8

Example ₆ is repeated with 1.0 gram of catalyst in accordance withExample 3. With a hydrogen peroxide conversion of 99% and acyclohexanone conversion of 67%, cyclohexanonoxime is formed withgreater than 99% selectivity, with reference to the cyclohexanoneconverted.

Example 9

Example 6 is repeated with 1.0 gram of catalyst in accordance withExample 4. With a hydrogen peroxide conversion of 99% and acyclohexanone conversion of 82%, cyclohexanonoxime is formed withgreater than 99% selectivity, with reference to the cyclohexanoneconverted.

Example 10

Example 6 is repeated with 0-66 grams of catalyst in accordance withExample 5. With a hydrogen peroxide conversion of 100% and acyclohexanone conversion of 81%, cyclohexanonoxime is formed with 86%selectivity, with reference to the cyclohexanone converted.

The following are examples of the epoxidation of 1-octene to give1-octene oxide using untreated catalyst (i.e., a catalyst which is nottreated with a base).

Example 11

1.6 grams of catalyst according to Example 1 in a mixture of 60 grams ofmethanol and 11.6 grams of 1-octane are initially introduced into a 100ml reactor with a double-walled jacket. The mixture is heated to 55° C.and 3.40 grams of 49 wt. % strength aqueous hydrogen peroxide solutionis added with stirring. After stirring for 30 minutes at 55° C., asample is withdrawn, filtered and analyzed. Unconverted hydrogenperoxide is determined by cerimetric titration, unconverted 1-octane andthe oxidation products 1-octane oxide, 1-methoxy-2-octanol and2-methoxy-1-octanol are determined using gas chromatography. With ahydrogen peroxide conversion of 29%, 66% of oxidation products areformed, with reference to the hydrogen peroxide converted. The epoxideselectivity, with reference to the oxidation products formed, is 74%.

Example 12

Example 11 is repeated using 1.1 grams of catalyst according to Example2. With a hydrogen peroxide conversion of 25%, 78% of oxidation productsare formed, with reference to hydrogen peroxide converted. The epoxideselectivity, with reference to the oxidation products formed, is 72%.

Example 13

Example 11 is repeated using 4.0 grams of catalyst according to Example3. With a hydrogen peroxide conversion of 34%, 67% of oxidation productsare formed, with reference to the hydrogen peroxide converted. Theepoxide selectivity, with reference to the oxidation products formed, is69%.

Example 14

Example 11 is repeated using 0.75 grams of catalyst according to Example4. With a hydrogen peroxide conversion of 21%, 53% of oxidation productsare formed, with reference to hydrogen peroxide converted. The epoxideselectivity, with reference to the oxidation products formed, is 44%.

Example 15

Example 11 is repeated using 0.66 grams of catalyst according to Example5. With a hydrogen peroxide conversion of 21%, 85% of oxidation productsare formed, with reference to the hydrogen peroxide converted. Theepoxide selectivity, with reference to the oxidation products formed, is88%.

The following examples relate to neutralizing the catalysts with sodiumacetate to thereby produce treated catalysts.

Example 16

5 grams of catalyst according to Example 1 are heated for 20 minutesunder reflux with a solution of 1 gram of sodium acetate in 100 ml ofdeionized water. This is then filtered, the catalyst is washed with hot,deionized water and with methanol, and dried in the air. A suspension of0.5 grams of the catalyst in 10 ml of deionized water had a pH of 3.7before neutralization, and a pH of 6.3 after neutralization.

Example 17

Example 16 is repeated with 5 grams of catalyst according to Example 2.A suspension of 0.5 grams of the catalyst in 10 ml of deionized waterhad a pH of 3.8 before neutralization and a pH of 6.5 afterneutralization.

Example 18

Example 16 is repeated with 5 grams of catalyst according to Example 3.A suspension of 0.5 grams of the catalyst in 10 ml of deionized waterhad a pH of 4.4 before neutralization, and a pH of 6.5 afterneutralization.

Example 19

Example 16 is repeated with 5 grams of catalyst according to Example 4.A suspension of 0.5 grams of the catalyst in 10 ml of deionized waterhad a pH of 3.8 before neutralization, and a pH of 6.6 afterneutralization.

Example 20

Example 16 is repeated with 5 grams of catalyst according to Example 5.A suspension of 0.5 grams of the catalyst in 10 ml of deionized waterhad a pH of 5.2 before neutralization, and a pH of 7.7 afterneutralization.

The following are examples of the epoxidation of 1-octane to give1-octane oxide using the neutralized catalysts (i.e., treatedcatalysts).

Example 21

Example 11 is repeated with 1.6 grams of the catalyst according toExample 16. With a hydrogen peroxide conversion of 30%, 84% of oxidationproducts are formed, with reference to the hydrogen peroxide converted.The epoxide selectivity, with reference to the oxidation productsformed, is 92%. Thus, the selectivity is higher than when usingnon-neutralized catalyst from Example 1 (see also Example 11).

Example 22

Example 11 is repeated with 1.l grams of the catalyst according toExample 17. With a hydrogen peroxide conversion of 29%, 85% of oxidationproducts are formed, with reference to the hydrogen peroxide converted.The epoxide selectivity, with reference to the oxidation productsformed, is 89%. Thus, the selectivity is higher than when usingnon-neutralized catalyst according to Example 2 (see also Example 12).

Example 23

Example 11 is repeated with 4.0 grams of the catalyst according toExample 18. With a hydrogen peroxide conversion of 35%, 92% of oxidationproducts are formed, with reference to the hydrogen peroxide converted.The epoxide selectivity, with reference to the oxidation productsformed, is 88%. Thus, the selectivity is higher than when usingnon-neutralized catalyst from Example 3 (see also Example 13).

Example 24

Example 11 is repeated with 0.76 grams of the catalyst according toExample 19. With a hydrogen peroxide conversion of 20%, 94% of oxidationproducts are formed, with reference to the hydrogen peroxide converted.The epoxide selectivity, with reference to the oxidation productsformed, is 91%. Thus, the selectivity is higher than when usingnon-neutralized catalyst from Example 4 (see also Example 14).

Example 25

Example 11 is repeated with 0.66 grams of the catalyst according toExample 20. With a hydrogen peroxide conversion of 26%, 100% ofoxidation products are formed, with reference to the hydrogen peroxideconverted. The epoxide selectivity, with reference to the oxidationproducts formed, is 98%.

By the expression "crystal structure of MFI or MEL", as used herein, ismeant structures of the type disclosed in U.S. Pat. No. 3,702,886 andMeier et al., Atlas of Zeolite Structure Types, supra.

While the invention has been described in terms of various specificexamples, those skilled in the art will appreciate that various changesand modifications may be made without departing from the spirit andscope of the invention, as defined in the claims.

The priority applications, German Patent Appl. Nos. P 43 23 255.8 and P44 19 195.2, filed in Germany on Jul. 12, 1993 and Jun. 1, 1994,respectively, are entirely incorporated herein by reference.

We claim:
 1. A process for preparing an oxime, comprising:reacting aketone with hydrogen peroxide and ammonia in a liquid phase in thepresence of a catalyst which includes catalyst particles with a corehaving a composition as follows:

    (SiO.sub.2).sub.x (AlO.sub.2).sub.y M.sub.y,

wherein x/y is in the range of 10 to 150, M represents a member selectedfrom the group consisting of: H, Na, K, NH₄, and NR₄, wherein R is analkyl group having 1 to 8 carbon atoms, and a shell over the core,wherein the shell has a composition as follows:

    (SiO.sub.2).sub.n (TiO.sub.2).sub.m,

wherein n/m is in the range of 12 to 1000, wherein both the core and theshell have a crystal structure of MFI or MEL; and recovering the oximeproduced in the reacting step.
 2. A process for preparing an oximeaccording to claim 1, wherein the shell of the catalyst has thecomposition (SiO₂)_(n) (TiO₂)_(m), wherein n/m is in the range of 20 to200.
 3. A process for preparing an oxime according to claim 1, whereinthe catalyst is present in the liquid phase as an aqueous suspensionwhich has a pH between 5 and
 9. 4. A process for preparing an oximeaccording to claim 2, wherein the catalyst is present in the liquidphase as an aqueous suspension which has a pH between 5 and 9.